Alkyl polyglycoside surfactants for use in subterranean formations

ABSTRACT

Methods and compositions for treating subterranean formations with treatment fluids comprising alkyl polyglycoside surfactants are provided. In one embodiment, the methods comprise providing a treatment fluid comprising an aqueous base fluid; and a surfactant comprising an alkyl polyglycoside or derivative thereof; introducing the treatment fluid into a wellbore penetrating at least a portion of a subterranean formation; and producing fluids from the wellbore during or subsequent to introducing the treatment fluid into the wellbore.

CROSS-REFERENCE TO RELATED APPLICATIONS

This is a continuation-in-part of U.S. application Ser. No. 15/763,757 entitled “Alkyl polyglycoside surfactants for use in subterranean formations,” filed Mar. 27, 2018, which is a U.S. National Stage Application of International Application No. PCT/US2015/060923 filed Nov. 16, 2015, each of which is herein incorporated by reference in its entirety.

BACKGROUND

The present disclosure relates to methods and compositions for treating subterranean formations, and more specifically, methods and compositions for treating subterranean formations with treatment fluids comprising surfactants.

Hydrocarbons, such as oil and gas, are commonly obtained from subterranean formations that may be located onshore or offshore. The development of subterranean operations and the processes involved in removing hydrocarbons from a subterranean formation typically involve a number of different steps such as, for example, drilling a wellbore at a desired well site, treating the wellbore to optimize production of hydrocarbons, and performing the necessary steps to produce and process the hydrocarbons from the subterranean formation.

Surfactants are widely used in treatment fluids for drilling operations and other well treatment operations, including hydraulic fracturing and acidizing (both fracture acidizing and matrix acidizing) treatments. Surfactants may also be used in enhanced or improved oil recovery operations. Many variables may affect the selection of a surfactant for use in such treatments and operations, such as interfacial surface tension, wettability, compatibility with other additives (such as other additives used in acidizing treatments), and emulsification tendency. Surfactants are an important component in treatment fluids for ensuring higher productivity from unconventional oil and gas formations. Surfactants may provide more effective fluid loss control, fluid flowback efficiency, and oil recovery. For example, surfactants may improve oil recovery by reducing interfacial tension, altering the wettability of the subterranean formation, and/or stabilizing an emulsion. However, conventional surfactants may present environmental, health, and safety concerns. In addition, conventional surfactants may be sensitive to changes in pH, temperature, and salinity.

BRIEF DESCRIPTION OF THE DRAWINGS

These drawings illustrate certain aspects of some of the embodiments of the present disclosure, and should not be used to limit or define the claims.

FIG. 1 is a diagram illustrating an example of a fracturing system that may be used in accordance with certain embodiments of the present disclosure.

FIG. 2 is a diagram illustrating an example of a subterranean formation in which a fracturing operation may be performed in accordance with certain embodiments of the present disclosure.

FIGS. 3A and 3B are graphs illustrating data relating to thermal stability of an alkyl polyglycoside formulation of the present disclosure and a field standard non-emulsifying surfactant formulation.

FIG. 4 is a series of photographs illustrating oil breaking through a formation sample in a column flow test.

FIGS. 5A and 5B are series of photographs illustrating emulsion break times for an alkyl polyglycoside formulation of the present disclosure and a field standard non-emulsifying surfactant formulation.

FIG. 6 is a graph illustrating data relating to pH and salinity stability of an alkyl polyglycoside formulation of the present disclosure.

While embodiments of this disclosure have been depicted, such embodiments do not imply a limitation on the disclosure, and no such limitation should be inferred. The subject matter disclosed is capable of considerable modification, alteration, and equivalents in form and function, as will occur to those skilled in the pertinent art and having the benefit of this disclosure. The depicted and described embodiments of this disclosure are examples only, and not exhaustive of the scope of the disclosure.

DESCRIPTION OF CERTAIN EMBODIMENTS

Illustrative embodiments of the present disclosure are described in detail herein. In the interest of clarity, not all features of an actual implementation may be described in this specification. It will of course be appreciated that in the development of any such actual embodiment, numerous implementation specific decisions may be made to achieve the specific implementation goals, which may vary from one implementation to another. Moreover, it will be appreciated that such a development effort might be complex and time consuming, but would nevertheless be a routine undertaking for those of ordinary skill in the art having the benefit of the present disclosure.

The present disclosure relates to methods and compositions for treating subterranean formations. Particularly, the present disclosure relates to methods and compositions for the use of alkyl polyglycoside surfactants in subterranean formations.

More specifically, the present disclosure provides treatment fluids comprising at least an aqueous base fluid and a surfactant comprising an alkyl polyglycoside or derivative thereof, and certain methods of use. In certain embodiments, the methods of the present disclosure comprise: providing a treatment fluid comprising: an aqueous base fluid and a surfactant comprising an alkyl polyglycoside or derivative thereof introducing the treatment fluid into a wellbore penetrating at least a portion of a subterranean formation; and producing fluids (e.g., hydrocarbons) from the wellbore during or subsequent to introducing the treatment fluid into the wellbore. In some embodiments, the treatment fluid may be introduced into a wellbore at or above a pressure sufficient to create or enhance one or more fractures in the subterranean formation. In some embodiments, the present disclosure provides a treatment composition comprising an aqueous base fluid; a surfactant comprising an alkyl polyglycoside or derivative thereof and a non-aromatic solvent selected from the group consisting of: an ethoxylated alcohol, an alkoxylated alcohol, a glycol ether, a disubstituted amide, a mixture of glycerine and acetone, isopropylidene glycerol, triethanolamine, ethylenediaminetetraacetic acid, N,N-dimethyl 9-decenamide, soya methyl ester, canola methyl ester, a mixture of methyl laurate and methyl myristate, a mixture of methyl soyate and ethyl lactate, any combination, and any derivative thereof.

Among the many potential advantages to the methods and compositions of the present disclosure, only some of which are alluded to herein, the methods and compositions of the present disclosure may provide surfactants for use in subterranean formations that are safer, less toxic, and/or more effective than certain other surfactants used in subterranean operations. Alkyl polyglycoside surfactants are non-toxic and biodegradable. Furthermore, alkyl polyglycoside surfactants may be more stable as they are less sensitive to temperature, pH, and salinity variations than conventional surfactants. In addition, alkyl polyglycoside surfactants are manufactured from plants and thus may be more commercially available. Another advantage may be a synergistic effect of an alkyl polyglycoside surfactant with other surfactants or solvents in the fluid, which may result in lower interfacial tension than the surfactants may achieve independently or without the solvents.

As used herein, the term “alkyl polyglycoside surfactant” refers to surfactants comprising an alkyl polyglycoside or derivatives thereof. Alkyl polyglycosides are a class of non-ionic surfactants. In certain embodiments, alkyl polyglycosides or derivatives thereof include at least one sugar group and at least one non-sugar group. When derived from glucose, alkyl polyglycosides are more specifically known as alkyl polyglucosides. Examples of alkyl polyglucosides that may be suitable for certain embodiments of the present disclosure include, but are not limited to compounds having the following general chemical structure, where m and n are non-zero integers:

The chemical structure of alkyl polyglycosides derived from other sugar molecules is similar, except for the difference in the type of sugar molecule on which the polyglycoside is based. In some embodiments, an alkyl polyglycoside or derivative thereof may be based on any suitable sugar molecule. For any type of alkyl polyglycoside, m may be in the range of 1 to 20, independent of the other parameters. In some embodiments, m may be in the range of 11 to 30, 15 to 30, or 20 to 30, independent of the other parameters. In certain embodiments, m may be 11 or higher, 15 or higher, or 20 or higher, independent of the other parameters. For any type of alkyl polyglycoside, n for the alkyl group may be in the range of 1 to 24, independent of the other parameters. In certain embodiments, the alkyl polyglycoside is an alkyl polyglucoside wherein m is in the range of 1 to 20 and n for the alkyl is in the range of 1 to 24. In certain embodiments, the alkyl polyglycoside surfactant of the present disclosure may include a combination of different compounds having this formula.

In some embodiments, the number of repeating sugar groups in an alkyl polyglycoside or derivative thereof may range from about 11 to about 30, from about 15 to about 30, or from about 20 to about 30. In certain embodiments, the alkyl polyglycoside or derivative thereof may include 11 or more, 15 or more, or 20 or more repeating sugar groups.

In some embodiments, the alkyl polyglycoside surfactant may have a molecular weight of about 3,000 g/mol or higher, 4,000 g/mol or higher, or 5,000 g/mol or higher. In certain embodiments, the molecular weight of the alkyl polyglycoside surfactant may be from about 3,000 g/mol to about 10,000 g/mol, from about 4,000 g/mol to about 10,000 g/mol, or from about 5,000 g/mol to about 10,000 g/mol.

In some embodiments, the methods and compositions of the present disclosure may comprise an alkyl polyglycoside derivative. Examples of suitable alkyl polyglycoside derivatives include, but are not limited to functionalized sulfonates, functionalized betaines, an inorganic salt of any of the foregoing. Specific examples of these alkyl polyglycoside surfactant derivatives may include, but are not limited to decyl polyglucoside hydroxypropylsulfonate sodium salt, lauryl polyglucoside hydroxypropylsulfonate sodium salt, coco polyglucoside hydroxypropylsulfonate sodium salt, lauryl polyglucoside sulfosuccinate disodium salt, decyl polyglucoside sulfosuccinate disodium salt, lauryl polyglucoside bis-hydroxyethylglycinate sodium salt, coco polyglucoside bis-hydroxyethylglycinate sodium salt, and any combination thereof. In some embodiments, a sulfonate alkyl polyglycoside may be a hydroxyalkylsulfonate. In some embodiments, the alkyl group of the hydroxylalkylsulfonate functionality is a short-chain alkyl group in the range of 1 to 6 carbons. Examples of suitable inorganic salt alkyl polyglycoside derivatives include, but are not limited to an inorganic salt of an alkali metal, an alkaline earth metal, and ammonium salts.

In certain embodiments, an alkyl polyglycoside or alkyl polyglycoside derivative surfactant may be present in a treatment fluid of the present disclosure in an amount from about 1×10⁻⁵ gallons per thousand gallons of treatment fluid (gpt) up to about 50 gpt. In some embodiments, the alkyl polyglycoside or alkyl polyglycoside derivative surfactant may be present in a treatment fluid of the present disclosure in an amount from about 0.1 gpt up to about 50 gpt. In some embodiments, the alkyl polyglycoside or alkyl polyglycoside derivative surfactant may be present in a treatment fluid of the present disclosure in an amount from about 0.1 gpt up to about 10 gpt.

In certain embodiments, additional surfactants may be used together with the alkyl polyglycoside surfactants. In some embodiments, the alkyl polyglycoside surfactant may have a synergistic effect with the additional surfactants. For example, the alkyl polyglycoside surfactant may help disperse the additives in the fluid. Examples of suitable additional surfactants include, but are not limited to ethoxylated amines, alkoxylated alkyl alcohols and salts thereof and alkoxylated alkyl phenols and salts thereof, alkyl and aryl sulfonates, sulfates, phosphates, carboxylates, polyoxyalkyl glycols, fatty alcohols, polyoxyethylene glycol sorbitan alkyl esters, sorbitan alkyl esters, polysorbates, glucosides, quaternary amine compounds, amine oxide surfactants, and any combination thereof.

In certain embodiments, surfactants of the present disclosure, either alone or in conjunction with other additives, may increase production of hydrocarbon fluids from hydrocarbon formations comprising unconventional reservoirs. Examples of unconventional reservoirs include, but are not limited to reservoirs such as tight sands, shale gas, shale oil, coalbed methane, tight carbonate, and gas hydrate reservoirs. Surfactants may affect many variables in subterranean treatments and operations, such as interfacial/surface tension, wettability, compatibility with other additives (such as other additives used in acidizing treatments), and emulsification tendency.

In certain embodiments, the surfactants of the present disclosure may comprise non-emulsifying surfactants, which may prevent emulsions from forming or reduce the emulsion tendency of fluids in the wellbore and in the subterranean formation, and may lower the risk of formation damage during production. In certain embodiments, the surfactants of the present disclosure may comprise weakly-emulsifying surfactants, which generate short-lived oil in water emulsion and make the interface more deformable and squeezable for the flow of oil droplets through tiny fractures in the subterranean formation, and may help to increase oil recovery in the reservoir.

In some embodiments, the surfactants of the present disclosure may act as a flowback aid. Flowback aids may reduce capillary pressure, oil blocks, and/or water blocks, improving the kinetics of flowback and minimizing the amount of fracturing fluid left behind in the formation. In addition, flowback aids may aid in the “clean up” of a proppant pack, and/or accelerate the flow of hydrocarbons through the formation and a proppant pack.

As used herein, a “water block” generally refers to a condition caused by an increase in water saturation in the near-wellbore area. A water block may form when the near-wellbore area is exposed to a relatively high volume of filtrate from the drilling fluid. In some embodiments, increased presence of water may cause clay present in the formation to swell and reduce permeability and/or the water may collect in pore throats, resulting in a decreased permeability due to increased capillary pressure and cohesive forces.

As used herein, an “oil block” generally refers to a condition in which an increased amount of oil saturates the area near the wellbore. Due to the wettability of the subterranean formation and the resulting capillary pressure, oil may reduce the permeability of the subterranean formation to the flow of fluids, including oil and water. Without limiting the disclosure to any particular theory or mechanism, it is believed that the compositions and methods described herein may remove a water or oil block by removing at least a portion of the water and/or oil in the near wellbore area and/or altering the wettability of the subterranean formation. For example, in certain embodiments, the formation surface may be oil wet. By altering the wettability of the surface of a subterranean formation to be more water wet, the surface of the formation may be more compatible with injection water and other water-based fluids. In certain embodiments, the methods and compositions of the present disclosure may also reduce interfacial tension between the fluid in the formation and the surfaces of the formation.

In some embodiments, the methods and compositions of the present disclosure may directly or indirectly reduce capillary pressure in the porosity of the formation. Reduced capillary pressure may lead to increased water and/or oil drainage rates. In some embodiments, improved water-drainage rates may allow a reduction in existing water blocks, as well as a reduction in the formation of water blocks. In certain embodiments, the methods and compositions of the present disclosure may allow for enhanced water, oil, and/or other fluid recovery.

In certain embodiments, a solvent may be used together with the alkyl polyglycoside surfactant. In some embodiments, the alkyl polyglycoside surfactant may have a synergistic effect with the solvent. In certain embodiments, a treatment fluid of the present disclosure may comprise an aqueous base fluid and a solvent. In some embodiments, this may result in lower interfacial tension than the alkyl polyglycoside surfactant or solvent may achieve independently. In certain embodiments, the solvent may comprise any suitable solvent or combination thereof. Examples of solvents suitable for some embodiments of the present disclosure include, but are not limited to a non-aqueous solvent, a non-aromatic solvent, an alcohol, glycerol, carbon dioxide, isopropanol, or any combination or derivative thereof. The non-aromatic solvents included in certain treatment fluids of the present disclosure may comprise any suitable non-aromatic solvent or combination thereof. In certain embodiments, a non-aromatic solvent may increase the effectiveness of an alkyl polyglycoside surfactant. Examples of non-aromatic solvents that may be suitable for use in certain embodiments of the present disclosure include, but are not limited to, an ethoxylated alcohol, an alkoxylated alcohol, a glycol ether, a disubstituted amide, RHODIASOLV® MSOL (a mixture of glycerine and acetone available from Solvay in Houston, Tex.), MUSOL® (isopropylidene glycerol, available from Halliburton in Houston, Tex.), triethanolamine, ethylenediaminetetraacetic acid, N,N-dimethyl 9-decenamide, soya methyl ester, canola methyl ester, STEPOSOL® C-42 (a mixture of methyl laurate and methyl myristate, available from Stepan in Northfield, Ill.), STEPOSOL® SC (a mixture of methyl soyate and ethyl lactate, available from Stepan in Northfield, Ill.), any combination, and any derivative thereof.

In some embodiments, the methods and compositions of the present disclosure may provide treatment fluids comprising surfactants that are more stable to variations in temperature, pH, and salinity than conventional surfactant compositions. For example, in some embodiments, the alkyl polyglycoside or alkyl polyglycoside derivative surfactant may provide stable interfacial tension across a variety of temperatures, pH levels, and salinities.

In certain embodiments of the present disclosure, alkyl polyglycoside surfactants, treatment fluids, or related additives of the present disclosure may be introduced into a subterranean formation, a wellbore penetrating a subterranean formation, tubing (e.g., pipeline), and/or a container using any method or equipment known in the art. Introduction of the alkyl polyglycoside surfactants, treatment fluids, or related additives of the present disclosure may in such embodiments include delivery via any of a tube, umbilical, pump, gravity, and combinations thereof. Additives, treatment fluids, or related compounds of the present disclosure may, in various embodiments, be delivered downhole (e.g., into the wellbore) or into top-side flowlines/pipelines or surface treating equipment.

The compositions used in the methods and compositions of the present disclosure may comprise any aqueous base fluid known in the art. The term “base fluid” refers to the major component of the fluid (as opposed to components dissolved and/or suspended therein), and does not indicate any particular condition or property of that fluids such as its mass, amount, pH, etc. Aqueous fluids that may be suitable for use in the methods and compositions of the present disclosure may comprise water from any source. Such aqueous fluids may comprise fresh water, salt water (e.g., water containing one or more salts dissolved therein), brine (e.g., saturated salt water), seawater, or any combination thereof. In most embodiments of the present disclosure, the aqueous fluids comprise one or more ionic species, such as those formed by salts dissolved in water. For example, seawater and/or produced water may comprise a variety of divalent cationic species dissolved therein. In certain embodiments, the density of the aqueous fluid can be adjusted, among other purposes, to provide additional particulate transport and suspension in the compositions of the present disclosure. In certain embodiments, the pH of the aqueous fluid may be adjusted (e.g., by a buffer or other pH adjusting agent) to a specific level, which may depend on, among other factors, the types of viscosifying agents, acids, and other additives included in the fluid. One of ordinary skill in the art, with the benefit of this disclosure, will recognize when such density and/or pH adjustments are appropriate.

In certain embodiments, the methods and compositions of the present disclosure optionally may comprise any number of additional additives. Examples of such additional additives include, but are not limited to, salts, additional surfactants, acids, proppant particulates, diverting agents, fluid loss control additives, gas, nitrogen, carbon dioxide, surface modifying agents, tackifying agents, foamers, corrosion inhibitors, scale inhibitors, catalysts, clay control agents, biocides, friction reducers, antifoam agents, bridging agents, flocculants, H₂S scavengers, CO₂ scavengers, oxygen scavengers, lubricants, viscosifiers, breakers, weighting agents, relative permeability modifiers, resins, wetting agents, coating enhancement agents, filter cake removal agents, antifreeze agents (e.g., ethylene glycol), and the like. A person skilled in the art, with the benefit of this disclosure, will recognize the types of additives that may be included in the fluids of the present disclosure for a particular application.

The alkyl polyglycoside surfactants and compositions of the present disclosure can be used in a variety of applications. These include downhole applications (e.g., drilling, fracturing, completions, oil production), use in conduits, containers, and/or other portions of refining applications, gas separation towers/applications, pipeline treatments, water disposal and/or treatments, and sewage disposal and/or treatments.

In some embodiments, the present disclosure provides methods for using the additives, treatment fluids, and related compounds to carry out a variety of subterranean treatments, including but not limited to hydraulic fracturing treatments, acidizing treatments, and drilling operations. In some embodiments, the compounds of the present disclosure may be used in treating a portion of a subterranean formation, for example, in acidizing treatments such as matrix acidizing or fracture acidizing. In certain embodiments, a treatment fluid may be introduced into a subterranean formation. In some embodiments, the treatment fluid may be introduced into a wellbore that penetrates a subterranean formation. In some embodiments, the treatment fluid may be introduced at a pressure sufficient to create or enhance one or more fractures within the subterranean formation (e.g., hydraulic fracturing).

Treatment fluids can be used in a variety of subterranean treatment operations. As used herein, the terms “treat,” “treatment,” “treating,” and grammatical equivalents thereof refer to any subterranean operation that uses a fluid in conjunction with achieving a desired function and/or for a desired purpose. Use of these terms does not imply any particular action by the treatment fluid. Illustrative treatment operations can include, for example, fracturing operations, gravel packing operations, acidizing operations, scale dissolution and removal, consolidation operations, and the like.

Certain embodiments of the methods and compositions disclosed herein may directly or indirectly affect one or more components or pieces of equipment associated with the preparation, delivery, recapture, recycling, reuse, and/or disposal of the disclosed compositions. For example, and with reference to FIG. 1, the disclosed methods and compositions may directly or indirectly affect one or more components or pieces of equipment associated with an exemplary fracturing system 10, according to one or more embodiments. In certain instances, the system 10 includes a fracturing fluid producing apparatus 20, a fluid source 30, a proppant source 40, and a pump and blender system 50 and resides at the surface at a well site where a well 60 is located. In certain instances, the fracturing fluid producing apparatus 20 combines a gel pre-cursor with fluid (e.g., liquid or substantially liquid) from fluid source 30, to produce a hydrated fracturing fluid that is used to fracture the formation. The hydrated fracturing fluid can be a fluid ready for use in a fracture stimulation treatment of the well 60 or a concentrate to which additional fluid is added prior to use in a fracture stimulation of the well 60. In some embodiments, the fracturing fluid producing apparatus 20 can be omitted and the fracturing fluid sourced directly from the fluid source 30. In certain embodiments, the fracturing fluid may comprise water, a hydrocarbon fluid, a polymer gel, foam, air, wet gases and/or other fluids.

The proppant source 40 can include a proppant for combination with the fracturing fluid. In certain embodiments, one or more treatment particulates of the present disclosure may be provided in the proppant source 40 and thereby combined with the fracturing fluid with the proppant. The system may also include additive source 70 that provides one or more additives (e.g., alkyl polyglycoside surfactants, gelling agents, weighting agents, and/or other additives) to alter the properties of the fracturing fluid. For example, the other additives 70 can be included to reduce pumping friction, to reduce or eliminate the fluid's reaction to the geological formation in which the well is formed, to operate as surfactants, and/or to serve other functions. In certain embodiments, the other additives 70 may include an alkyl polyglycoside or alkyl polyglycoside surfactant of the present disclosure.

The pump and blender system 50 receives the fracturing fluid and combines it with other components, including proppant from the proppant source 40 and/or additional fluid from the additives 70. The resulting mixture may be pumped down the well 60 under a pressure sufficient to create or enhance one or more fractures in a subterranean zone, for example, to stimulate production of fluids from the zone. Notably, in certain instances, the fracturing fluid producing apparatus 20, fluid source 30, and/or proppant source 40 may be equipped with one or more metering devices (not shown) to control the flow of fluids, proppant particles, and/or other compositions to the pumping and blender system 50. Such metering devices may permit the pumping and blender system 50 to source from one, some or all of the different sources at a given time, and may facilitate the preparation of fracturing fluids in accordance with the present disclosure using continuous mixing or “on-the-fly” methods. Thus, for example, the pumping and blender system 50 can provide just fracturing fluid into the well at some times, just proppant particles at other times, and combinations of those components at yet other times.

FIG. 2 shows the well 60 during a fracturing operation in a portion of a subterranean formation of interest 102 surrounding a wellbore 104. The wellbore 104 extends from the surface 106, and the fracturing fluid 108 is applied to a portion of the subterranean formation 102 surrounding the horizontal portion of the wellbore. Although shown as vertical deviating to horizontal, the wellbore 104 may include horizontal, vertical, slant, curved, and other types of wellbore geometries and orientations, and the fracturing treatment may be applied to a subterranean zone surrounding any portion of the wellbore. The wellbore 104 can include a casing 110 that is cemented or otherwise secured to the wellbore wall. The wellbore 104 can be uncased or include uncased sections. Perforations can be formed in the casing 110 to allow fracturing fluids and/or other materials to flow into the subterranean formation 102. In cased wells, perforations can be formed using shape charges, a perforating gun, hydro jetting and/or other tools.

The well is shown with a work string 112 depending from the surface 106 into the wellbore 104. The pump and blender system 50 is coupled a work string 112 to pump the fracturing fluid 108 into the wellbore 104. The working string 112 may include coiled tubing, jointed pipe, and/or other structures that allow fluid to flow into the wellbore 104. The working string 112 can include flow control devices, bypass valves, ports, and or other tools or well devices that control a flow of fluid from the interior of the working string 112 into the subterranean zone 102. For example, the working string 112 may include ports adjacent the wellbore wall to communicate the fracturing fluid 108 directly into the subterranean formation 102, and/or the working string 112 may include ports that are spaced apart from the wellbore wall to communicate the fracturing fluid 108 into an annulus in the wellbore between the working string 112 and the wellbore wall.

The working string 112 and/or the wellbore 104 may include one or more sets of packers 114 that seal the annulus between the working string 112 and wellbore 104 to define an interval of the wellbore 104 into which the fracturing fluid 108 will be pumped. FIG. 2 shows two packers 114, one defining an uphole boundary of the interval and one defining the downhole end of the interval. When the fracturing fluid 108 is introduced into wellbore 104 (e.g., in FIG. 2, the area of the wellbore 104 between packers 114) at a sufficient hydraulic pressure, one or more fractures 116 may be created in the subterranean zone 102. The proppant particulates (and/or treatment particulates of the present disclosure) in the fracturing fluid 108 may enter the fractures 116 where they may remain after the fracturing fluid flows out of the wellbore. These proppant particulates may “prop” fractures 116 such that fluids may flow more freely through the fractures 116.

While not specifically illustrated herein, the disclosed methods and compositions may also directly or indirectly affect any transport or delivery equipment used to convey the compositions to the fracturing system 10 such as, for example, any transport vessels, conduits, pipelines, trucks, tubulars, and/or pipes used to fluidically move the compositions from one location to another, any pumps, compressors, or motors used to drive the compositions into motion, any valves or related joints used to regulate the pressure or flow rate of the compositions, and any sensors (i.e., pressure and temperature), gauges, and/or combinations thereof, and the like.

To facilitate a better understanding of the present disclosure, the following examples of certain aspects of preferred embodiments are given. The following examples are not the only examples that could be given according to the present disclosure and are not intended to limit the scope of the disclosure or claims.

EXAMPLES Example 1

In this example, the thermal stability of an alkyl polyglycoside (“APG”) formulation was compared to a field standard non-emulsifying surfactant formulation. Thermal stability was tested by measuring the interfacial tensions of each composition at three different conditions: (1) at room temperature, (2) after heating and maintaining the composition at 320° F. and 300 psi for 1 day, and (3) after heating and maintaining the composition at 320° F. and 300 psi for 4 days. Interfacial tension measurements were obtained using a “Tracker H” Teclis Instruments automated drop tensiometer. FIGS. 3A and 3B show the interfacial tension measurements for each formulation at each condition. Table 1 shows the final interfacial tension for each formulation at each condition. As shown in FIGS. 3A and 3B and Table 1, the APG formulation was more stable to temperature variation than the field standard non-emulsifying surfactant formulation.

TABLE 1 Interfacial Tension (mN/m) 1 day at 4 days at Room 320° F. 320° F. Surfactant Formulation Temperature & 300 psi & 300 psi Field Standard Non- 25.5 33.0 30.0 Emulsifying Surfactant Formulation APG Surfactant Formulation 27.8 28.9 28.6

Example 2

In this example, a column flow test was performed to compare the time taken for a sample of crude oil from a Permian basin well to break through a 40/60 mesh sand formation sample treated with an APG surfactant formulation and to break through a 40/60 mesh sand formation sample treated with a field standard non-emulsifying surfactant formulation. FIG. 4 shows the experimental setup of the column flow test and oil breaking through the formation sample. The results of the column flow tests and the chemical scoring index (“CSI”) score for each formulation are shown in Table 3. The results show that crude oil broke through the formation sample treated with the APG formulation faster than it broke through the formation sample treated with the field standard non-emulsifying surfactant formation.

TABLE 2 Time taken for oil break Surfactant Formulation CSI Score through (min) Field Standard Non- 45 24 Emulsifying Surfactant Formulation APG Surfactant Formulation 15 17

Example 3

In this example, an emulsion tendency test was performed to compare the emulsion tendency of an APG formulation in a 10% broken gel to a field standard non-emulsifying surfactant formulation in a 10% broken gel at room temperature and at 60° C. FIGS. 5A and 5B show the experimental setup and results of the emulsion tendency test for the APG surfactant formulation (labeled “LS1” in each image) and the field standard non-emulsifying surfactant formulation (labeled “0” in each image). Each formulation was mixed and observed to determine how long after mixing the emulsion broke at each temperature. The results of the emulsion tendency test are shown in Table 3. As shown in FIGS. 5A and 5B and Table 3, the emulsion break time for the APG formulation was comparable to the field standard non-emulsifying surfactant formulation.

TABLE 3 Emulsion Break Time (s) Surfactant Formulation Room Temperature 60° C. Field Standard Non- 57 21 Emulsifying Surfactant Formulation APG Surfactant Formulation 104 29

Example 4

In this example, pH and salinity stability was measured for an alkyl polyglycoside formulation. Alkyl polyglycoside formulations comprising varying concentrations of NaCl (1 wt %, 3 wt %, and 6 wt %) were prepared at three different pH levels (4, 7, and 10), and surface tension was measured for each. The results of the surface tension measurements are shown in FIG. 6, which shows that surface tension of the alkyl polyglycoside formulation was relatively stable with respect to pH and salinity variations.

An embodiment of the present disclosure is a method comprising: providing a treatment fluid comprising: an aqueous base fluid; and a surfactant comprising an alkyl polyglycoside or derivative thereof; introducing the treatment fluid into a wellbore penetrating at least a portion of a subterranean formation; and producing fluids from the wellbore during or subsequent to introducing the treatment fluid into the wellbore.

Another embodiment of the present disclosure is a composition comprising: an aqueous base fluid; a surfactant comprising an alkyl polyglycoside or derivative thereof; and a non-aromatic solvent selected from the group consisting of: an ethoxylated alcohol, an alkoxylated alcohol, a glycol ether, a disubstituted amide, a mixture of glycerine and acetone, isopropylidene glycerol, triethanolamine, ethylenediaminetetraacetic acid, N,N-dimethyl 9-decenamide, soya methyl ester, canola methyl ester, any combination, and any derivative thereof.

Another embodiment of the present disclosure is a method comprising: providing a treatment fluid comprising: an aqueous base fluid; and a surfactant comprising an alkyl polyglycoside or derivative thereof and introducing the treatment fluid into a wellbore penetrating at least a portion of a subterranean formation at or above a pressure sufficient to create or enhance one or more fractures in the subterranean formation

Therefore, the present disclosure is well adapted to attain the ends and advantages mentioned as well as those that are inherent therein. The particular embodiments disclosed above are illustrative only, as the present disclosure may be modified and practiced in different but equivalent manners apparent to those skilled in the art having the benefit of the teachings herein. While numerous changes may be made by those skilled in the art, such changes are encompassed within the spirit of the subject matter defined by the appended claims. Furthermore, no limitations are intended to the details of construction or design herein shown, other than as described in the claims below. It is therefore evident that the particular illustrative embodiments disclosed above may be altered or modified and all such variations are considered within the scope and spirit of the present disclosure. In particular, every range of values (e.g., “from about a to about b,” or, equivalently, “from approximately a to b,” or, equivalently, “from approximately a-b”) disclosed herein is to be understood as referring to the power set (the set of all subsets) of the respective range of values. The terms in the claims have their plain, ordinary meaning unless otherwise explicitly and clearly defined by the patentee. 

What is claimed is:
 1. A method comprising: providing a treatment fluid comprising: an aqueous base fluid; a surfactant comprising an alkyl polyglycoside or derivative thereof having a molecular weight of about 5,000 g/mol to 10,000 g/mol and comprising 20 to 30 repeating sugars; and a solvent selected from the group consisting of an ethoxylated alcohol, an alkoxylated alcohol, a disubstituted amide, a mixture of glycerine and acetone, isopropylidene glycerol, triethanolamine, ethylenediaminetetraacetic acid, N,N-dimethyl 9-decenamide, soya methyl ester, canola methyl ester, a mixture of methyl laurate and methyl myristate, a mixture of methyl soyate and ethyl lactate, any combination thereof, and any derivative thereof; introducing the treatment fluid into a wellbore penetrating at least a portion of a subterranean formation containing one or more proppant packs; and producing fluids from the wellbore during or subsequent to introducing the treatment fluid into the wellbore, wherein the fluids travel from the subterranean formation through the one or more proppant packs.
 2. The method of claim 1, further comprising: allowing the surfactant to reduce capillary pressure in at least a portion of the subterranean formation.
 3. The method of claim 1, further comprising: allowing the surfactant to alter a wettability of a surface of the formation.
 4. The method of claim 1, further comprising: allowing the surfactant to reduce interfacial tension between a fluid in the formation and a surface of the formation.
 5. The method of claim 1, further comprising: allowing the surfactant to remove at least a portion of an oil block, a water block, or both.
 6. The method of claim 1, wherein the amount of fluids produced from the wellbore during or subsequent to introducing the treatment fluid is greater than the amount of fluids that would be produced during or subsequent to introducing the same treatment fluid without the surfactant.
 7. The method of claim 1, wherein the surfactant comprises an alkyl polyglycoside derivative selected from the group consisting of: a functionalized sulfonate, a functionalized betaine, an inorganic salt of any of the foregoing, and any combination thereof.
 8. The method of claim 1, wherein the surfactant is present in the treatment fluid in an amount from about 1×10⁻⁵ gpt up to about 50 gpt based on the total volume of the treatment fluid.
 9. The method of claim 1, wherein the treatment fluid further comprises an additional surfactant.
 10. A composition comprising: an aqueous base fluid; a surfactant comprising an alkyl polyglycoside or derivative thereof having a molecular weight of about 5,000 g/mol to 10,000 g/mol and comprising 20 to 30 repeating sugars; and a non-aromatic solvent selected from the group consisting of an ethoxylated alcohol, an alkoxylated alcohol, a disubstituted amide, a mixture of glycerine and acetone, isopropylidene glycerol, triethanolamine, ethylenediaminetetraacetic acid, N,N-dimethyl 9-decenamide, soya methyl ester, canola methyl ester, a mixture of methyl laurate and methyl myristate, a mixture of methyl soyate and ethyl lactate, any combination thereof, and any derivative thereof.
 11. The composition of claim 10, wherein the surfactant is present in the composition in an amount from about 1×10⁻⁵ gpt up to about 50 gpt based on the total volume of the composition.
 12. The composition of claim 10, wherein the surfactant comprises an alkyl polyglycoside derivative selected from the group consisting of: a functionalized sulfonate, a functionalized betaine, an inorganic salt of any of the foregoing, and any combination thereof.
 13. A method comprising: providing a treatment fluid comprising: an aqueous base fluid; a surfactant comprising an alkyl polyglycoside or derivative thereof having a molecular weight of about 5,000 g/mol to 10,000 g/mol and comprising 20 to 30 repeating sugars; and a solvent selected from the group consisting of an ethoxylated alcohol, an alkoxylated alcohol, a disubstituted amide, a mixture of glycerine and acetone, isopropylidene glycerol, triethanolamine, ethylenediaminetetraacetic acid, N,N-dimethyl 9-decenamide, soya methyl ester, canola methyl ester, a mixture of methyl laurate and methyl myristate, a mixture of methyl soyate and ethyl lactate, any combination thereof, and any derivative thereof; introducing the treatment fluid into a wellbore penetrating at least a portion of a subterranean formation at or above a pressure sufficient to create or enhance one or more fractures in the subterranean formation.
 14. The method of claim 13, further comprising: producing fluids from the wellbore.
 15. The method of claim 13, wherein the surfactant comprises an alkyl polyglycoside derivative selected from the group consisting of: a functionalized sulfonate, a functionalized betaine, an inorganic salt of any of the foregoing, and any combination thereof.
 16. The method of claim 13, wherein the surfactant is present in the treatment fluid in an amount from about 1×10⁻⁵ gpt up to about 50 gpt based on the total volume of the treatment fluid.
 17. The method of claim 13, wherein the treatment fluid further comprises an additional surfactant. 